JPH05230525A - Fused salt chamber integrated with sludge remover - Google Patents
Fused salt chamber integrated with sludge removerInfo
- Publication number
- JPH05230525A JPH05230525A JP4069180A JP6918092A JPH05230525A JP H05230525 A JPH05230525 A JP H05230525A JP 4069180 A JP4069180 A JP 4069180A JP 6918092 A JP6918092 A JP 6918092A JP H05230525 A JPH05230525 A JP H05230525A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- molten salt
- fused salt
- cylinder
- removing device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、溶融塩槽とスラッジ除
去装置とが一体となった金属熱処理中に生ずる塩浴中の
スラッジを連続的に効率良く除去できる溶融塩槽に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a molten salt tank in which a molten salt tank and a sludge removing device are integrated and which is capable of continuously and efficiently removing sludge generated in a salt bath during metal heat treatment.
【0002】[0002]
【従来の技術及びその問題点】溶融塩による金属の熱処
理を行うと、経時的に溶融塩中にスラッジが発生し、処
理部品の品質に悪影響を及ぼすため、これを除去する必
要がある。従来、一般的には、操業を停止し、溶融塩槽
底部に沈降したり、浴中に浮遊しているスラッジを金属
製の金網で捕集除去したり、槽底部に沈めた皿状の容器
(スラッジパン)中に捕集又は沈降させ、この皿を静か
に持ち上げ、これを除去するか、操業を停止せず、連続
的に溶融塩槽からポンプにより汲み上げ、別に用意した
スラッジ除去装置の中でスラッジを除去し、スラッジ除
去後の溶融塩を槽に戻す方法が行われている。2. Description of the Related Art When a metal is heat-treated with a molten salt, sludge is generated in the molten salt over time, which adversely affects the quality of treated parts. Therefore, it is necessary to remove the sludge. Conventionally, in general, operation is stopped, sedimentation at the bottom of the molten salt tank, sludge floating in the bath is collected and removed with a metal wire mesh, and a dish-shaped container is sunk at the bottom of the tank. (Sludge pan) to collect or settle, gently lift this dish and remove it, or continuously pump it up from the molten salt tank without stopping the operation, in a separately prepared sludge removal device Is used to remove sludge, and the molten salt after sludge removal is returned to the tank.
【0003】連続的なスラッジ除去方法については、溶
融塩槽とは別設したスラッジ除去装置を用いたスラッジ
除去装置が特願昭55−29134号公報に記載されて
いる。しかしながら、この公報記載の発明では、循環す
るための塩浴槽とスラッジ除去槽の配管が溶融塩浴中に
含まれる溶融温度の高い、例えば炭酸ナトリウム等が徐
々に配管に沈着し、配管を閉塞し、場合によっては除去
装置から溶融塩があふれるおそれがあり、危険である。
このような現象は週末の設備停止により、まず凝固分離
した高溶融温度成分が配管外周に沈着したり、又は処理
部品を溶融塩槽に投入したとき、槽内の溶融塩温度が低
下し、高溶融温度成分が析出し、配管に沈着するため
に、操業中に徐々に生ずる。しかしながら、このような
環境は実操業では避けられず、またこの高溶融温度成分
の沈着防止策として、配管を保温、ヒーター加熱して
も、配管の閉塞を監視しながら操業する必要があるた
め、設備管理の点で非常に非能率的である。また、配管
の沈着物は配管を加熱するか、取外し、蒸気洗浄等によ
り洗浄しなければならず、保守に長時間を要する。Regarding a continuous sludge removing method, a sludge removing device using a sludge removing device provided separately from the molten salt tank is described in Japanese Patent Application No. 55-29134. However, in the invention described in this publication, the piping of the salt bath and the sludge removal tank for circulation has a high melting temperature contained in the molten salt bath, for example, sodium carbonate or the like gradually deposits on the piping and blocks the piping. In some cases, molten salt may overflow from the removing device, which is dangerous.
Such a phenomenon is caused by a high melting temperature component that is solidified and separated on the outer periphery of the pipe due to the equipment being stopped on the weekend, or when the treated parts are put into the molten salt tank, the molten salt temperature in the tank decreases and The melting temperature component precipitates and deposits on the pipe, so that it gradually occurs during operation. However, such an environment is unavoidable in actual operation, and as a measure to prevent the deposition of this high melting temperature component, it is necessary to operate while monitoring the blockage of the pipe even if the pipe is kept warm and the heater is heated. Very inefficient in terms of facility management. In addition, deposits on the pipe must be cleaned by heating or removing the pipe and cleaning with steam, which requires a long time for maintenance.
【0004】本発明は、配管への高溶融温度成分の沈着
を可及的に減少させ、もって高能率にスラッジ除去を行
える溶融塩槽を提供することを目的とする。It is an object of the present invention to provide a molten salt tank which can reduce the deposition of high melting temperature components on piping as much as possible, and can remove sludge with high efficiency.
【0005】[0005]
【問題点を解決するための手段】本発明は、溶融塩浴槽
本体上部の一部をなし、溶融塩浴と一体となった除滓ス
ペース部とその中に配置される脱着可能な除滓エレメン
トからなるスラッジ除去装置を一体化した溶融塩槽によ
り、前記課題を解決したものである。本発明において、
前記スラッジ除去装置は、溶融塩槽とは別の独立した加
熱手段及び温度制御機器を具えることができる。また、
前記スラッジ除去装置は、溶融塩槽からポンプで汲み上
げられ首振り可能な供給管から供給される溶融塩を沈静
化するために中央に配置された静置筒と、その静置筒底
部に固定されたスラッジ受け皿と、静置筒外周に嵌合す
る内筒及びその下端がスラッジ受け皿に嵌合し上部外周
に溶融塩の還流する小孔が開けられた外筒と、これら内
筒及び外筒間に前記外筒の小孔部より下から前記内筒の
上部に向かって傾斜して設けられた傾斜板とを備えたも
のとすることができる。これら溶融塩槽において、前記
スラッジ除去装置及び溶融塩浴槽は純チタン又はニッケ
ル合金製の厚板を加工して製作されたものとし、さらに
前記除滓エレメントは純チタン又はニッケル合金により
製作されたものとしてもよい。DISCLOSURE OF THE INVENTION The present invention is directed to a slag space portion which is part of the upper portion of the molten salt bath main body and is integrated with the molten salt bath, and a removable slag element disposed therein. The above-mentioned problems are solved by a molten salt tank in which a sludge removing device consisting of is integrated. In the present invention,
The sludge removing device may include a heating means and a temperature control device which are independent of the molten salt tank. Also,
The sludge removing device is a stationary tube arranged in the center for calming the molten salt pumped from the molten salt tank and supplied from a swingable supply pipe, and is fixed to the bottom of the stationary tube. Sludge pan, an inner cylinder fitted to the outer circumference of the stationary cylinder, an outer cylinder with its lower end fitted to the sludge pan, and a small hole in the upper outer circumference where molten salt circulates, and between these inner cylinder and outer cylinder And an inclined plate that is inclined from below the small hole portion of the outer cylinder toward the upper portion of the inner cylinder. In these molten salt tanks, the sludge removing device and the molten salt bath shall be manufactured by processing a thick plate made of pure titanium or nickel alloy, and the slag element shall be made of pure titanium or nickel alloy. May be
【0006】[0006]
【作用】本発明の溶融塩槽はスラッジ除去装置が一体化
されているため、溶融塩槽からポンプで汲み上げられた
溶融塩をスラッジ除去装置に供給する供給管を従来のス
ラッジ除去装置を溶融塩槽を別設する場合に比べて短く
することができ、炉本体、炉本体と一体となったスラッ
ジ除去装置からの伝熱、輻射熱により加熱されるため、
特別な手段を講じなくとも供給管中に高溶融温度成分が
沈着することがなくなる。さらにはスラッジ除去後の溶
融塩は除滓エレメントの小孔から直接溶融塩槽に還流す
るため溶融塩の戻り管が不要となる。また、スラッジ除
去装置及び溶融塩浴槽を純チタン又はニッケル合金製の
厚板を加工して製作されたものとすれば、従来のような
ライニング構造のものに比べ加熱源からの溶融塩への電
熱効果が著しく向上する。さらに除滓エレメントを純チ
タン又はニッケル合金により製作されたものとすれば、
除滓エレメントに溶融塩の付着が少なくなり小孔の目詰
りも防止される。Since the sludge removing device is integrated in the molten salt tank of the present invention, a supply pipe for supplying the molten salt pumped up from the molten salt tank to the sludge removing device is provided with a conventional sludge removing device. It can be shortened compared to the case where a tank is installed separately, and because it is heated by heat transfer and radiant heat from the furnace body and the sludge removal device integrated with the furnace body,
The high melting temperature component is not deposited in the supply pipe without taking any special measures. Further, since the molten salt after sludge removal is directly returned to the molten salt tank through the small holes of the slag element, a molten salt return pipe is unnecessary. Further, if the sludge removing device and the molten salt bath are manufactured by processing a thick plate made of pure titanium or nickel alloy, electric heat from the heating source to the molten salt is higher than that of the conventional lining structure. The effect is significantly improved. Further, if the slag element is made of pure titanium or nickel alloy,
Molten salt adherence to the slag element is reduced and clogging of small holes is prevented.
【0007】以下に添付図面を参照して本発明の実施例
を説明する。図1は、本発明に係る溶融塩槽の一例を示
すものであり、この図1において、1は溶融塩槽、2は
スラッジ除去装置の加熱ヒーター、3はスラッジ除去装
置の加熱制御手段、4はスラッジ除去装置本体、5は除
滓エレメント、6はポンプに接続された首振り可能な溶
融塩供給管、7は溶融塩加熱源、8は溶融塩炉殻、9は
熱電対をそれぞれ示す。このように本発明の溶融塩槽
は、所謂溶融塩槽本体上部の一部をなし、溶融塩浴と一
体となった除滓スペース部とその中に配置される脱着可
能な除滓エレメントからなるスラッジ除去装置を一体化
して構成されるものである。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows an example of a molten salt tank according to the present invention. In FIG. 1, 1 is a molten salt tank, 2 is a heater for a sludge removing device, 3 is heating control means for a sludge removing device, 4 Is a sludge removing apparatus main body, 5 is a slag element, 6 is a molten salt supply pipe which can be swung, connected to a pump, 7 is a molten salt heating source, 8 is a molten salt furnace shell, and 9 is a thermocouple. As described above, the molten salt tank of the present invention forms a part of the so-called molten salt tank main body, and comprises a slag space portion integrated with the molten salt bath and a removable slag element disposed therein. The sludge removing device is integrated.
【0008】図2は、除滓スペース部に配置される着脱
可能な除滓エレメントの一例を一部切り欠いて示すもの
であり、また図3はその斜視透視図である。これら図2
及び図3において、除滓エレメント5の中央部には、静
置筒11が配置され、この静置筒11の下部には開口部
13が設けられ、そして底部にはその外周に小孔21が
明けられたスラッジ受け皿16が固定されている。静置
筒11の外周には内筒15が嵌入され、またスラッジ受
け皿16にはその上部外周に小孔20が明けられた外筒
10が嵌入されており、これら内筒15、外筒10の間
に前記外筒10の小孔20部より下から前記内筒15の
上部に向かって傾斜して設けられた傾斜板14が設けら
れている。これにより、除滓エレメント5自体が除滓ス
ペースから着脱可能とされるとともに除滓エレメント5
の内筒15、外筒10及び傾斜板14が一体となって静
置筒11から分離可能とされる。FIG. 2 shows an example of a removable slag element disposed in the slag space part with a part cut away, and FIG. 3 is a perspective perspective view thereof. These Figure 2
In FIG. 3, a stationary tube 11 is arranged in the center of the slag element 5, an opening 13 is provided in the lower part of the stationary tube 11, and a small hole 21 is formed in the outer periphery of the bottom thereof. The opened sludge tray 16 is fixed. An inner cylinder 15 is fitted on the outer circumference of the stationary cylinder 11, and an outer cylinder 10 having a small hole 20 is fitted on the outer circumference of the upper part of the sludge receiving tray 16. The inner cylinder 15 and the outer cylinder 10 are An inclined plate 14 is provided between the small holes 20 of the outer cylinder 10 and the upper part of the inner cylinder 15 so as to be inclined. As a result, the slag element 5 itself can be detached from the slag space and the slag element 5 can be removed.
The inner cylinder 15, the outer cylinder 10 and the inclined plate 14 can be integrally separated from the stationary cylinder 11.
【0009】除滓エレメント5はエレメントの寿命、取
り扱い易さ、効果を考えると、耐熱性、耐食性が十分で
あり、軽量で小さなスペースで溶融塩の流通経路が長
く、スラッジ分離効果の良いことが求められる。そのた
め、薄板でこれら性能を十分に発揮でき、入手の容易な
金属で構成することが好ましく、具体的には純チタン、
ニッケル合金が良い。また溶融塩槽をライニングとする
代わりに厚肉の板を使用することにより、加熱源からの
溶融塩への電熱効果が著しく向上する利点も得られる。
除滓エレメント5は溶融塩と常に接触するため、化学反
応、及び侵食をうける結果、エレメント自体が酸化、窒
化、浸炭等の影響があると、外筒10表面が剥離したス
ケールにより、又はエレメント表面肌荒れにより溶融塩
中のスラッジが付着しやすくなるため、外筒10に穿孔
された小孔20の目詰りが生じるおそれがある。このた
めにもエレメントは純チタン、ニッケル合金のような化
学的に極めて安定な金属で製作することが好ましい。Considering the life of the element, easiness of handling, and effect, the slag element 5 has sufficient heat resistance and corrosion resistance, is lightweight and has a long molten salt flow path in a small space, and has a good sludge separation effect. Desired. Therefore, it is preferable that these properties can be sufficiently exhibited in a thin plate and that the metal is easily available. Specifically, pure titanium,
Nickel alloy is good. Further, by using a thick plate instead of using the molten salt tank as a lining, there is an advantage that the electric heating effect from the heating source to the molten salt is significantly improved.
Since the slag element 5 is constantly in contact with the molten salt, if the element itself is affected by oxidation, nitriding, carburizing, etc. as a result of being subjected to chemical reaction and erosion, the scale on which the surface of the outer cylinder 10 is peeled off or the element surface Sludge in the molten salt is likely to adhere due to rough skin, so that the small holes 20 formed in the outer cylinder 10 may be clogged. For this reason, the element is preferably made of a chemically extremely stable metal such as pure titanium or nickel alloy.
【0010】本発明において、傾斜板14はエレメント
中の溶融塩流通経路を長くし、スラッジがこの経路内で
分離しやすくするために設けられるものである。本発明
では、さらにスラッジ分離効果を高めるため、例えば特
願昭55−29134号公報に開示されているように、
繊維状細線を丸めて塊状としたスラッジ補集部材を収納
した除滓エレメント中に溶融塩浴槽内の溶融塩を循環さ
せて溶融塩中のスラッジを分離するようにしてもよい。
また、傾斜板14の上及び下にスラッジの性質に応じて
捕集部材をセットするようにしてもよい。In the present invention, the inclined plate 14 is provided to lengthen the molten salt flow passage in the element and to facilitate sludge separation in this passage. In the present invention, in order to further enhance the sludge separation effect, for example, as disclosed in Japanese Patent Application No. 55-29134,
The sludge in the molten salt may be separated by circulating the molten salt in the molten salt bath through the slag element containing the sludge collecting member formed by rolling the fibrous thin wire into a lump.
Further, a collecting member may be set above and below the inclined plate 14 according to the property of sludge.
【0011】このようにな除滓エレメント5の静置筒1
1内へ、溶融塩槽のスラッジを含んだ溶融塩をポンプで
汲み上げ供給管6から供給する。溶融塩は静置筒11内
でスラッジ成分が沈降し開口部13から内外筒間の除滓
スペースへと送られる。スラッジ成分はスラッジ受け皿
16に沈降し、傾斜板14間をさらに上方へと移送され
る間にスラッジ成分がほぼ完全にスラッジ受け皿14に
沈降し、スラッジが除去された溶融塩は外筒10上部の
小孔20から滲みだし、直接溶融塩浴槽に還流される。
かくして、このような操作を繰返した後、スラッジ受け
皿16にスラッジがたまったら、供給管6の先端を回動
させ、静置筒11及びスラッジ受け皿16を残し、内筒
15、傾斜板14及び外筒10を上方に引き抜く。この
時、溶融塩はスラッジ受け皿16に設けられた小孔21
から溶融塩浴槽へ戻り、スラッジはそのままスラッジ受
け皿16に残り、このスラッジはスラッジ受け皿16の
底部に設けられたスラッジ栓12から除去される。その
後、内筒15、外筒10、傾斜板14、静置筒11、ス
ラッジ栓等を水洗、乾燥し、場合によっては、補集部材
をセットして、繰返し使用する。In this way, the stationary cylinder 1 of the slag element 5 is
Molten salt containing sludge in the molten salt tank is pumped into the inside of 1 by a pump and supplied from a supply pipe 6. The sludge component of the molten salt settles in the stationary cylinder 11 and is sent from the opening 13 to the slag space between the inner and outer cylinders. The sludge component settles in the sludge pan 16 and the sludge component is almost completely settled in the sludge pan 14 while being transferred between the inclined plates 14 and the molten salt from which the sludge has been removed is in the upper part of the outer cylinder 10. It exudes from the small holes 20 and is directly returned to the molten salt bath.
Thus, after repeating such an operation, when sludge is accumulated in the sludge receiving tray 16, the tip of the supply pipe 6 is rotated to leave the stationary tube 11 and the sludge receiving tray 16, and the inner tube 15, the inclined plate 14 and the outer tube. Pull the tube 10 upward. At this time, the molten salt is discharged into the small holes 21 provided in the sludge tray 16.
Then, the sludge returns to the molten salt bath, and the sludge remains in the sludge tray 16 as it is, and the sludge is removed from the sludge plug 12 provided at the bottom of the sludge tray 16. After that, the inner cylinder 15, the outer cylinder 10, the inclined plate 14, the stationary cylinder 11, the sludge plug, etc. are washed with water and dried, and in some cases, a collecting member is set and repeatedly used.
【0012】これら操作時において、溶融塩槽と一体化
した除滓エレメントは溶融塩槽とは独立した加熱手段及
び温度制御手段を備え、これらにより独立した熱管理を
行っても良い。During these operations, the slag element integrated with the molten salt tank may be provided with a heating means and a temperature control means independent of the molten salt tank, and independent heat management may be performed by these.
【0013】次に、図示した構成の鉄系部品の塩浴浸炭
窒化処理槽を用いて、その効果を試験した。直径1000m
m、深さ1500mmのスラッジ除去装置を備えた溶融塩浴槽
中に、アルカリシアン酸、アルカリ炭酸塩混合溶融塩を
溶解し、580℃に保持し、除滓エレメントを稼働させ
た。この中にグロス約350kgの炭素鋼製シャフトを投入
し、90分保持を1工程とし、7時間で3工程繰り返し
た。溶融塩は800L/Hの流速で除滓エレメントに供給
したところ、3工程後の処理品質は窒化層15〜20μ、ポ
ーラス層1/3と良好であり、また水不溶解分として約
1000gのスラッジを補集することができた。また、2mm
のチタン材を12mmのステンレス鋼製溶融塩外槽にライニ
ングした場合に比べ、12mmのニッケル基合金製の場合、
部品投入後580℃に昇温するのに15分短縮できた。Next, the effect was tested using a salt bath carbonitriding tank for iron-based parts having the illustrated construction. Diameter 1000m
In a molten salt bath equipped with a sludge removing device having a depth of 1500 mm and a sludge removing device, a molten salt containing a mixture of alkali cyanic acid and an alkali carbonate was dissolved and kept at 580 ° C. to operate the slag element. A carbon steel shaft having a gross weight of about 350 kg was put therein, and holding for 90 minutes was set as one step, and three steps were repeated for 7 hours. When the molten salt was supplied to the slag element at a flow rate of 800 L / H, the treatment quality after the three steps was as good as the nitriding layer 15 to 20μ and the porous layer 1/3, and the water insoluble content was about
It was possible to collect 1000 g of sludge. Also, 2 mm
Compared to the case where the titanium material of 12 mm is lined in a 12 mm stainless steel molten salt outer tank, in the case of 12 mm nickel-based alloy,
It took 15 minutes to raise the temperature to 580 ° C after the parts were put in.
【0014】[0014]
【発明の効果】以上のような本発明によれば、溶融塩の
供給管長さが短くてすみ、供給管の目詰りが減少し、さ
らには溶融塩の戻り管が省略されるため、戻り管内の目
詰り等を考慮する必要がなくなり、構成が簡単になり、
保守管理が大幅に簡略化され、金属の熱処理品質を高品
質に維持し得る溶融塩のスラッジ除去が連続して簡単に
行えるという効果を有する。As described above, according to the present invention, the length of the molten salt supply pipe is short, clogging of the supply pipe is reduced, and the molten salt return pipe is omitted. There is no need to consider clogging of the
This has the effect that maintenance management is greatly simplified and sludge removal of molten salt that can maintain the heat treatment quality of metal at high quality can be performed continuously and easily.
【図1】本発明に係る溶融塩槽の概略説明図である。FIG. 1 is a schematic explanatory view of a molten salt tank according to the present invention.
【図2】本発明に係る除滓エレメントの一例を一部切り
欠いて示す説明図である。FIG. 2 is an explanatory view showing an example of a slag element according to the present invention with a part cut away.
【図3】図2に示した除滓エレメントの一例の斜視透視
図である。3 is a perspective perspective view of an example of the slag element shown in FIG. 2. FIG.
1 溶融塩槽 2 加熱ヒーター 3 加熱制御手段 4 スラッジ除去装置本体 5 除滓エレメント 6 供給管 7 溶融塩加熱源 8 溶融塩炉殻 9 熱電対 10 外筒 11 静置筒 12 スラッジ栓 13 開口部 14 傾斜板 15 内筒 16 スラッジ受け皿 20 小孔 21 小孔 DESCRIPTION OF SYMBOLS 1 Molten salt tank 2 Heating heater 3 Heating control means 4 Sludge removing device main body 5 Slag element 6 Supply pipe 7 Molten salt heating source 8 Molten salt furnace shell 9 Thermocouple 10 Outer cylinder 11 Stationary cylinder 12 Sludge plug 13 Opening 14 Inclined plate 15 Inner cylinder 16 Sludge tray 20 Small hole 21 Small hole
Claims (5)
塩浴と一体となった除滓スペース部とその中に配置され
る脱着可能な除滓エレメントからなるスラッジ除去装置
を一体化した溶融塩槽。1. A sludge removing device, which forms a part of the upper portion of the molten salt bath main body and is integrated with a molten salt bath, and a sludge removing device including a removable sludge element disposed therein. Molten salt tank.
別の独立した加熱手段及び温度制御機器を具えた請求項
1記載の溶融塩槽。2. The molten salt tank according to claim 1, wherein the sludge removing device includes a heating means and a temperature control device which are independent of the molten salt tank.
ポンプで汲み上げられ首振り可能な供給管から供給され
る溶融塩を沈静化するために中央に配置された静置筒
と、その静置筒底部に固定されたスラッジ受け皿と、静
置筒外周に嵌合する内筒及びその下端がスラッジ受け皿
に嵌合し上部外周に溶融塩の還流する小孔が開けられた
外筒と、これら内筒及び外筒間に前記外筒の小孔部より
下から前記内筒の上部に向かって傾斜して設けられた傾
斜板とを備えた請求項1又は2記載の溶融塩槽。3. A stationary cylinder, wherein the sludge removing device is arranged in the center for calming the molten salt pumped from a molten salt tank and supplied from a swingable supply pipe, and its stationary state. A sludge tray fixed to the bottom of the tube, an inner tube fitted to the outer circumference of the stationary tube and an outer tube having a lower end fitted to the sludge tray and a small hole through which molten salt circulates on the outer circumference of the inner tube. The molten salt tank according to claim 1 or 2, further comprising: an inclined plate provided between the cylinder and the outer cylinder so as to incline from a lower portion of the outer cylinder toward an upper portion of the inner cylinder.
純チタン又はニッケル合金製の厚板を加工して製作され
たものである請求項1乃至3記載の溶融塩槽。4. The molten salt tank according to claim 1, wherein the sludge removing device and the molten salt bath are manufactured by processing a thick plate made of pure titanium or nickel alloy.
ケル合金により製作されたものである請求項3記載の溶
融塩槽。5. The molten salt tank according to claim 3, wherein the slag element is made of pure titanium or nickel alloy.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06918092A JP3280691B2 (en) | 1992-02-18 | 1992-02-18 | Molten salt tank with integrated sludge removal device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06918092A JP3280691B2 (en) | 1992-02-18 | 1992-02-18 | Molten salt tank with integrated sludge removal device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05230525A true JPH05230525A (en) | 1993-09-07 |
JP3280691B2 JP3280691B2 (en) | 2002-05-13 |
Family
ID=13395270
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP06918092A Expired - Lifetime JP3280691B2 (en) | 1992-02-18 | 1992-02-18 | Molten salt tank with integrated sludge removal device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3280691B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07308519A (en) * | 1994-05-17 | 1995-11-28 | Honda Motor Co Ltd | Device for removing sludge and its production |
US5527018A (en) * | 1994-01-13 | 1996-06-18 | Durferrit Gmbh Thermotechnik | Filter unit and apparatus for desludging salt baths |
JP2018187555A (en) * | 2017-05-01 | 2018-11-29 | パーカー熱処理工業株式会社 | Sludge separation apparatus |
US20210198141A1 (en) * | 2019-12-26 | 2021-07-01 | Samsung Display Co., Ltd. | Glass substrate chemical strengthening furnace apparatus |
CN113264648A (en) * | 2021-05-28 | 2021-08-17 | 安洁士环保(上海)股份有限公司 | Continuous fused salt heat conduction oil sludge thermal desorption device |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50146567A (en) * | 1974-05-16 | 1975-11-25 | ||
JPS55161064A (en) * | 1979-03-22 | 1980-12-15 | Degussa | Method and apparatus for removing sludge from salt bath |
JPS56127176A (en) * | 1980-03-10 | 1981-10-05 | Paakaa Netsushiyori Kogyo Kk | Sludge removal from melted salt bath |
JPS57117800U (en) * | 1981-01-16 | 1982-07-21 |
-
1992
- 1992-02-18 JP JP06918092A patent/JP3280691B2/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50146567A (en) * | 1974-05-16 | 1975-11-25 | ||
JPS55161064A (en) * | 1979-03-22 | 1980-12-15 | Degussa | Method and apparatus for removing sludge from salt bath |
JPS56127176A (en) * | 1980-03-10 | 1981-10-05 | Paakaa Netsushiyori Kogyo Kk | Sludge removal from melted salt bath |
JPS57117800U (en) * | 1981-01-16 | 1982-07-21 |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5527018A (en) * | 1994-01-13 | 1996-06-18 | Durferrit Gmbh Thermotechnik | Filter unit and apparatus for desludging salt baths |
JPH07308519A (en) * | 1994-05-17 | 1995-11-28 | Honda Motor Co Ltd | Device for removing sludge and its production |
US6723240B1 (en) | 1994-05-17 | 2004-04-20 | Honda Giken Kogyo Kabushiki Kaisha | Sludge removing device |
JP2018187555A (en) * | 2017-05-01 | 2018-11-29 | パーカー熱処理工業株式会社 | Sludge separation apparatus |
US20210198141A1 (en) * | 2019-12-26 | 2021-07-01 | Samsung Display Co., Ltd. | Glass substrate chemical strengthening furnace apparatus |
US11952309B2 (en) * | 2019-12-26 | 2024-04-09 | Samsung Display Co., Ltd. | Glass substrate chemical strengthening furnace apparatus |
CN113264648A (en) * | 2021-05-28 | 2021-08-17 | 安洁士环保(上海)股份有限公司 | Continuous fused salt heat conduction oil sludge thermal desorption device |
Also Published As
Publication number | Publication date |
---|---|
JP3280691B2 (en) | 2002-05-13 |
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